CN108368564B - Method for fixing arsenic and arsenic-containing glass solidified body - Google Patents
Method for fixing arsenic and arsenic-containing glass solidified body Download PDFInfo
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- CN108368564B CN108368564B CN201680073830.4A CN201680073830A CN108368564B CN 108368564 B CN108368564 B CN 108368564B CN 201680073830 A CN201680073830 A CN 201680073830A CN 108368564 B CN108368564 B CN 108368564B
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- calcium arsenate
- copper
- arsenate
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- 229910052785 arsenic Inorganic materials 0.000 title claims abstract description 112
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 title claims abstract description 111
- 239000011521 glass Substances 0.000 title claims abstract description 58
- 238000000034 method Methods 0.000 title claims abstract description 52
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 78
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 67
- RMBBSOLAGVEUSI-UHFFFAOYSA-H Calcium arsenate Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-][As]([O-])([O-])=O.[O-][As]([O-])([O-])=O RMBBSOLAGVEUSI-UHFFFAOYSA-H 0.000 claims abstract description 62
- 229940103357 calcium arsenate Drugs 0.000 claims abstract description 62
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 37
- 239000000463 material Substances 0.000 claims abstract description 33
- 229910052742 iron Inorganic materials 0.000 claims abstract description 32
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 72
- 238000002386 leaching Methods 0.000 claims description 36
- 239000003513 alkali Substances 0.000 claims description 20
- 239000007788 liquid Substances 0.000 claims description 19
- 238000004017 vitrification Methods 0.000 claims description 18
- 239000010802 sludge Substances 0.000 claims description 17
- MHUWZNTUIIFHAS-XPWSMXQVSA-N 9-octadecenoic acid 1-[(phosphonoxy)methyl]-1,2-ethanediyl ester Chemical compound CCCCCCCC\C=C\CCCCCCCC(=O)OCC(COP(O)(O)=O)OC(=O)CCCCCCC\C=C\CCCCCCCC MHUWZNTUIIFHAS-XPWSMXQVSA-N 0.000 claims description 15
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 15
- 239000000920 calcium hydroxide Substances 0.000 claims description 15
- 235000011116 calcium hydroxide Nutrition 0.000 claims description 15
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 15
- 229940047047 sodium arsenate Drugs 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 14
- 239000011734 sodium Substances 0.000 claims description 14
- MKOYQDCOZXHZSO-UHFFFAOYSA-N [Cu].[Cu].[Cu].[As] Chemical compound [Cu].[Cu].[Cu].[As] MKOYQDCOZXHZSO-UHFFFAOYSA-N 0.000 claims description 12
- 239000011575 calcium Substances 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 12
- 230000003647 oxidation Effects 0.000 claims description 12
- 238000007254 oxidation reaction Methods 0.000 claims description 12
- 238000000926 separation method Methods 0.000 claims description 12
- JEMGLEPMXOIVNS-UHFFFAOYSA-N arsenic copper Chemical compound [Cu].[As] JEMGLEPMXOIVNS-UHFFFAOYSA-N 0.000 claims description 9
- 239000007800 oxidant agent Substances 0.000 claims description 8
- 239000000706 filtrate Substances 0.000 claims description 6
- 230000003100 immobilizing effect Effects 0.000 claims description 4
- 235000012239 silicon dioxide Nutrition 0.000 claims description 3
- 239000010949 copper Substances 0.000 description 34
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 32
- 229910052802 copper Inorganic materials 0.000 description 32
- 239000000243 solution Substances 0.000 description 32
- 235000011121 sodium hydroxide Nutrition 0.000 description 22
- 238000010828 elution Methods 0.000 description 17
- 239000002699 waste material Substances 0.000 description 17
- 239000002893 slag Substances 0.000 description 14
- UYZMAFWCKGTUMA-UHFFFAOYSA-K iron(3+);trioxido(oxo)-$l^{5}-arsane;dihydrate Chemical compound O.O.[Fe+3].[O-][As]([O-])([O-])=O UYZMAFWCKGTUMA-UHFFFAOYSA-K 0.000 description 11
- 238000003723 Smelting Methods 0.000 description 9
- 230000001590 oxidative effect Effects 0.000 description 8
- 239000002244 precipitate Substances 0.000 description 8
- 239000012670 alkaline solution Substances 0.000 description 7
- 230000007613 environmental effect Effects 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000002002 slurry Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 230000002829 reductive effect Effects 0.000 description 4
- 239000004576 sand Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 229910052787 antimony Inorganic materials 0.000 description 3
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 3
- VETKVGYBAMGARK-UHFFFAOYSA-N arsanylidyneiron Chemical compound [As]#[Fe] VETKVGYBAMGARK-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 230000036961 partial effect Effects 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- DJHGAFSJWGLOIV-UHFFFAOYSA-N Arsenic acid Chemical compound O[As](O)(O)=O DJHGAFSJWGLOIV-UHFFFAOYSA-N 0.000 description 2
- 229910017251 AsO4 Inorganic materials 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 2
- 239000005751 Copper oxide Substances 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- IKWTVSLWAPBBKU-UHFFFAOYSA-N a1010_sial Chemical compound O=[As]O[As]=O IKWTVSLWAPBBKU-UHFFFAOYSA-N 0.000 description 2
- 229940000488 arsenic acid Drugs 0.000 description 2
- 229910000413 arsenic oxide Inorganic materials 0.000 description 2
- 229960002594 arsenic trioxide Drugs 0.000 description 2
- GCPXMJHSNVMWNM-UHFFFAOYSA-N arsenous acid Chemical compound O[As](O)O GCPXMJHSNVMWNM-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 229910000431 copper oxide Inorganic materials 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- -1 for example Chemical compound 0.000 description 2
- 150000002506 iron compounds Chemical class 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- DJHGAFSJWGLOIV-UHFFFAOYSA-K Arsenate3- Chemical compound [O-][As]([O-])([O-])=O DJHGAFSJWGLOIV-UHFFFAOYSA-K 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- JJLJMEJHUUYSSY-UHFFFAOYSA-L Copper hydroxide Chemical compound [OH-].[OH-].[Cu+2] JJLJMEJHUUYSSY-UHFFFAOYSA-L 0.000 description 1
- 239000005750 Copper hydroxide Substances 0.000 description 1
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 229940000489 arsenate Drugs 0.000 description 1
- HAYXDMNJJFVXCI-UHFFFAOYSA-N arsenic(5+) Chemical compound [As+5] HAYXDMNJJFVXCI-UHFFFAOYSA-N 0.000 description 1
- 229910052797 bismuth Inorganic materials 0.000 description 1
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 229910052681 coesite Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229940030341 copper arsenate Drugs 0.000 description 1
- 229910001956 copper hydroxide Inorganic materials 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- RKYSWCFUYJGIQA-UHFFFAOYSA-H copper(ii) arsenate Chemical compound [Cu+2].[Cu+2].[Cu+2].[O-][As]([O-])([O-])=O.[O-][As]([O-])([O-])=O RKYSWCFUYJGIQA-UHFFFAOYSA-H 0.000 description 1
- 229910052906 cristobalite Inorganic materials 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229910052682 stishovite Inorganic materials 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 229910052905 tridymite Inorganic materials 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/20—Agglomeration, binding or encapsulation of solid waste
- B09B3/25—Agglomeration, binding or encapsulation of solid waste using mineral binders or matrix
- B09B3/29—Agglomeration, binding or encapsulation of solid waste using mineral binders or matrix involving a melting or softening step
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/006—Wet processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/58—Treatment of water, waste water, or sewage by removing specified dissolved compounds
- C02F1/62—Heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C1/00—Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
- C03C1/002—Use of waste materials, e.g. slags
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C3/00—Glass compositions
- C03C3/04—Glass compositions containing silica
- C03C3/062—Glass compositions containing silica with less than 40% silica by weight
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/04—Extraction of metal compounds from ores or concentrates by wet processes by leaching
- C22B3/12—Extraction of metal compounds from ores or concentrates by wet processes by leaching in inorganic alkaline solutions
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
- C22B3/22—Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B30/00—Obtaining antimony, arsenic or bismuth
- C22B30/04—Obtaining arsenic
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/103—Arsenic compounds
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
- C25C1/12—Electrolytic production, recovery or refining of metals by electrolysis of solutions of copper
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
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- Water Supply & Treatment (AREA)
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- General Life Sciences & Earth Sciences (AREA)
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- Treatment Of Sludge (AREA)
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Abstract
The present invention provides a method for fixing arsenic, which is characterized in that arsenic is made into a glass solidified body by adding calcium arsenate to a vitrified material containing iron, silica and an alkaline component so that the weight ratio of iron to silica is 0.5 to 0.9 and the alkaline component amount is 14 to 26 wt%.
Description
Technical Field
The present invention relates to a method for fixing arsenic to produce a glass solidified body in which the amount of arsenic eluted is limited to or below environmental standards, and an arsenic-containing glass solidified body. More particularly, the present invention relates to an arsenic fixing method capable of limiting the amount of arsenic eluted to an environmental standard or less by forming calcium arsenate recovered from a smelting intermediate or the like into a glass solidified body, and an arsenic-containing glass solidified body obtained by the method. The method for fixing arsenic according to the present invention is suitable as a method for treating copper-containing arsenic sludge or the like produced in a copper smelting process.
This application claims priority based on 2015, 12, 23, japanese application patent application No. 2015-250760, and the contents thereof are incorporated herein.
Background
In the electrolytic smelting of copper, copper and arsenic are gradually accumulated in the electrolyte. Thus extracting a portion of the electrolyte for liquid purification treatment. Extracting copper (Cu) containing arsenic during the liquid purification treatment3As, etc.). The copper arsenide-containing sludge contains approximately 40-60 mass% of copper and 20-40 mass% of arsenic, and contains 0.5-5 mass% of lead, tin, antimony, bismuth, and the like, respectively. Accordingly, after removing impurities such as arsenic, the copper arsenide-containing sludge is returned to the copper smelting process, and the copper component is recovered from the copper arsenide-containing sludge. On the other hand, since impurities such as arsenic are gradually accumulated in the copper smelting system and adversely affect the quality of copper, the impurities such as arsenic are removed to the outside of the system.
As a method of removing arsenic contained in copper arsenide-containing sludge or the like to the outside of a copper smelting system by performing a treatment of fixing the arsenic to a stable compound, for example, the following treatment method has been known.
In the method disclosed in patent document 1, first, alkaline oxidation leaching is performed in a heated state by adding a sodium hydroxide solution to a copper-arsenic-containing material and blowing air.Then, after the completion of leaching, the pH of the liquid to be treated is adjusted to pH7.5 to 10, and the liquid is separated into a leaching residue containing a copper component and a solution containing arsenic. Then, a ferric iron compound is added to the arsenic-containing solution so that the Fe/As molar ratio is 0.9 to 1.1 to form a FeAs precipitate, and the FeAs precipitate recovered by the solid-liquid separation is mixed with a sulfuric acid solution to prepare an acidic slurry or an acidic solution. Then, the slurry or the solution is subjected to a heat treatment to produce crystalline scorodite (FeAsO)4·2H2O) to fix arsenic.
In the method disclosed in patent document 2, first, arsenous acid (As) is extracted from arsenic-containing soot leaching water in a heated state2O3). Next, an oxidizing agent (e.g., manganese peroxide) and hydrated lime are added to the filtrate to react with each other, thereby producing and recovering calcium arsenate. Subsequently, the calcium arsenate was mixed with recycled glass frit and melted at 1200 ℃ to produce an arsenic-containing glass solidified body.
In the method disclosed in patent document 3, first, sodium-based alkaline residue containing arsenic and antimony is heated to 850 to 1200 ℃ to selectively reduce and separate antimony generated from a carbon-based reducing agent. Next, a glass component was added to the remaining sodium arsenate and heated and melted to produce a solidified glass of arsenic.
In the method disclosed in non-patent document 1, CaO-SiO is added at 1400 ℃ under a constant oxygen partial pressure2The slag and calcium arsenate are heated and melted to produce a solidified glass of arsenic.
Patent document 1: japanese patent laid-open publication No. 2014-208581
Patent document 2: international publication No. WO2014/059535A1
Patent document 3: chinese patent publication No. CN102965517A gazette
Non-patent document 1: paper presented at GDMB sensor "slurries in Metallurgiy" P.M. SWASH et al.Aachen, Germany, 17-19March, 1999.
The treatment method of patent document 1 has the following advantages: arsenic is fixed as scorodite, the arsenic concentration in scorodite is high, and the conversion efficiency from the iron arsenic precipitate of the intermediate product to scorodite is also good. On the other hand, since an expensive divalent iron salt is used for the formation of the iron-arsenic precipitate, the cost tends to increase. Further, since the adhered arsenic is removed by washing with water after the synthesis of scorodite, an arsenic-containing waste liquid is generated, which increases the cost of treatment. Further, since scorodite has a bulk specific gravity of about 1 and is small, disposal of scorodite in a scorodite state imposes a burden on the volume of a treatment site.
In the treatment method of patent document 2, the step of leaching water from arsenic-containing soot to filter an arsenous acid solution and adding magnesium oxide and hydrated lime to the solution to produce calcium arsenate is time-consuming and costly. And there is a problem that the arsenic contained in the glass solidified body is insufficiently fixed.
The treatment method of patent document 3 is a method of glass-curing sodium arsenate, and since arsenic oxide is volatilized at a temperature of 1000 ℃ or higher, it is difficult to treat exhaust gas.
In the treatment method of non-patent document 1, CaO-SiO is used2The slag vitrification of calcium arsenate at a constant oxygen partial pressure requires appropriate control of the oxygen partial pressure, and thus has a problem of difficulty in practical operation.
Disclosure of Invention
The present invention provides a method for fixing arsenic glass, which solves the above-mentioned problems of the conventional methods, and an arsenic-containing glass solidified body obtained by the method. According to the present invention, it is possible to realize efficient and easy glass immobilization of arsenic and to reduce the elution amount of arsenic contained in a glass-solidified body to an environmental standard or less.
The present invention relates to a method for fixing arsenic and an arsenic-containing glass solidified body having the following structures (hereinafter, referred to as "method for fixing arsenic according to the present invention" and "arsenic-containing glass solidified body according to the present invention").
[1] A method for fixing arsenic, characterized in that arsenic is made into a glass-solidified body by adding calcium arsenate to a vitrification material containing iron, silica and an alkaline component so that the weight ratio of iron to silica is 0.5 to 0.9 and the alkaline component is 14 to 26 wt%.
[2] the method for immobilizing arsenic according to the above [1], wherein an alkaline solution and an oxidizing agent are added to a copper-arsenic-containing material to perform oxidative leaching, the leaching residue is subjected to solid-liquid separation, slaked lime is added to the recovered alkaline solution of arsenic acid to generate calcium arsenate, and the vitrified material is added to the recovered calcium arsenate so that the weight ratio of iron to silica and the amount of the alkaline component are obtained, thereby producing a glass-solidified body of calcium arsenate.
[3] the method for fixing arsenic according to [2], wherein the copper-arsenic-containing material is a copper-arsenic-containing sludge, sodium hydroxide and an oxidizing agent are added to the copper-arsenic-containing sludge, arsenic is leached by heating, the leaching residue is subjected to solid-liquid separation, slaked lime is added to the recovered sodium arsenate solution to produce calcium arsenate, and the vitrified material is added to the recovered calcium arsenate so that the weight ratio of iron to silica and the amount of the alkaline component are achieved, thereby producing a glass-solidified calcium arsenate.
[ 4 ] the method for immobilizing arsenic according to [3], wherein calcium arsenate is produced by adding slaked lime to a sodium arsenate solution, and the solution containing calcium arsenate is subjected to solid-liquid separation to recover calcium arsenate, while the filtrate containing sodium hydroxide is returned to the oxidation leaching step and reused as an alkali source for the oxidation leaching.
[ 5 ] an arsenic-containing glass-hardened material characterized by containing 5 to 15 wt% of arsenic, 0.5 to 0.9 wt% of iron and 0.9 wt% of silica, and an alkali component Na2The total amount of O and CaO is 14 to 26 wt.%.
The glass solidified body produced by the arsenic fixing method of the present invention can be stored as a mold for a long period of time, and therefore can be stored stably without scattering like scorodite, which is powder.
According to the arsenic fixing method of the present invention, the arsenic concentration in the solidified glass can be increased to 13 wt% or more in the solidified glass using waste glass, and the arsenic concentration in the solidified glass can be increased to 11 wt% or more in the solidified glass using copper slag. Since these glass-solidified bodies are smaller in volume than scorodite, the limited volume of the final treatment site can be effectively utilized.
In the method for fixing arsenic according to the present invention, calcium arsenate produced by adding hydrated lime to the sodium arsenate solution can be used while recovering sodium arsenate by oxidative leaching using sodium hydroxide. In this case, since sodium hydroxide is generated together with the generation of calcium arsenate, most of the sodium hydroxide can be returned to the leaching step and reused. Therefore, sodium hydroxide can be used effectively, and the consumption amount thereof can be reduced.
The method for fixing arsenic according to the present invention is a method for fixing calcium arsenate by vitrification, and is not a method for treating iron-arsenic precipitates generated by adding a trivalent iron compound to an alkaline solution of arsenic acid as in the conventional method, and therefore, the treatment cost can be reduced without using an expensive trivalent iron compound.
Unlike scorodite, the arsenic-containing glass solidified body produced by the arsenic fixing method of the present invention does not require washing with water, and the waste liquid has a low arsenic content, so that the burden of waste liquid treatment is small.
Further, in many cases, the waste glass contains a small amount of arsenic, and therefore is difficult to recover and reuse, and most of the waste glass is buried, but according to the arsenic fixing method of the present invention, since the arsenic concentration of the solidified glass can be increased, the limited volume of the final treatment site can be effectively used as compared with the case where the waste glass is buried.
Drawings
Fig. 1 is a process diagram showing a treatment process according to the present invention.
Detailed Description
Embodiments of the method for fixing arsenic and the arsenic-containing glass solidified body according to the present invention will be described below.
The method for fixing arsenic according to the present invention is characterized in that calcium arsenate is added to a vitrified material containing iron, silica and an alkaline component so that the weight ratio of iron to silica is 0.5 to 0.9 and the amount of the alkaline component is 14 to 26 wt%, thereby forming a glass-solidified body from arsenic.
As the calcium arsenate, for example, calcium arsenate produced by adding slaked lime to an alkaline arsenate solution recovered by oxidizing leaching a copper-arsenic-containing material with an alkaline solution and an oxidizing agent added thereto can be used. The copper-arsenic-containing material may be, for example, a copper-arsenic-containing sludge produced in copper electrolytic smelting. As the alkaline solution, a sodium hydroxide solution can be used.
The method comprises recovering and washing copper arsenide-containing sludge produced in copper electrolytic smelting, adding sodium hydroxide to a ph of 7.5 or more, adding an oxidizing agent to the sludge, heating the mixture to leach arsenic, subjecting the leachate to solid-liquid separation to recover a sodium arsenate solution, and adding hydrated lime to the sodium arsenate solution to produce calcium arsenate. As the calcium arsenate used in the method for fixing arsenic according to the present invention, calcium arsenate recovered from a copper arsenide-containing sludge solution produced in the electrolytic copper refining can be used. Hereinafter, a process of recovering calcium arsenate from a copper arsenide-containing sludge solution and vitrifying the calcium arsenate will be described. This step is shown in fig. 1.
[ alkaline oxidizing leaching procedure ]
An alkaline solution and an oxidizing agent are added to the copper arsenide-containing sludge to leach out arsenic. In the alkaline oxidative leaching, the pH of the solution is preferably 7.5 or more. As the oxidizing agent, air, oxygen, chlorine compounds, and the like can be used. Air and oxygen may be blown into the solution in the state of microbubbles. The heating temperature of the oxidative leaching is preferably 90 ℃ or lower.
In the oxidation leaching using a sodium hydroxide solution as an alkaline solution, copper arsenide is oxidized in the sodium hydroxide solution, copper forms copper oxide or copper hydroxide as a solid residue, and arsenic forms sodium arsenate and is leached in the solution, as shown in the following formula [1 ].
2Cu3As+4NaOH+4O2＝3Cu2O↓+2Na2HAsO4+H2O [1]
In the region where the pH of the alkaline oxidative leach is less than 7.5, for example, a trace amount of copper ions and arsenic (V) ions react to form copper arsenate [ Cu ]3(AsO4)2Thus, the arsenic concentration in the solution is reduced. Since arsenic leaching is performed when pH is adjusted to 7.5 or more by adding sodium hydroxide, it is preferable to perform oxidation leaching while adjusting pH to 7.5 or more.
As shown in the above reaction formula [1], since 2 moles of sodium hydroxide are required for the oxidative leaching of 1 mole of arsenic, the amount of NaOH to be added may be adjusted so that the NaOH/As molar ratio is 2 times (1 equivalent). When the arsenic concentration in the raw material is clear, the total amount of sodium hydroxide may be added in a required amount at the start of leaching. In this case, even when the liquid property at the initial stage of leaching is strongly alkaline (about pH 14), when the pH at the end of leaching is set to a range of 7.5 to 10, the concentration of heavy metal ions such as copper and lead is limited, and an arsenic leachate containing arsenic (V) of high purity can be obtained.
The leaching temperature is preferably 30 to 90 ℃, and if the temperature is lower than 30 ℃, the leaching time is longer, and if the temperature is higher than 90 ℃, the amount of generated steam is increased, which causes waste of heating cost.
According to the alkaline oxidation leaching, arsenic is selectively leached from the copper arsenide-containing sludge, and the separation property from metals coexisting with copper, lead, and the like contained in the sludge is good. Moreover, the slurry after leaching has good filterability, and can be filtered in a short time. In addition, the quality of copper contained in the leaching residue is as high as 80-85%, and copper smelting treatment is easy to perform.
[ procedure for producing calcium arsenate ]
And (3) carrying out solid-liquid separation on the leachate obtained by the alkaline oxidation leaching, thereby removing leaching residues containing copper oxide, and recovering the sodium arsenate solution of the filtrate. If slaked lime is added to the sodium arsenate solution, the following formula [2]]As shown, calcium arsenate (As) is generated3Ca5O13H) In that respect Recovering the calcium arsenate.
3Na2HAsO4+5Ca(OH)2＝6NaOH+As3Ca5O13H↓+3H2O [2]
In the calcium arsenate-producing step, As shown in the above reaction formula [2], the amount of slaked lime produced from calcium arsenate may be added in an amount such that the Ca/As molar ratio is from 1.7 to 2.0, since the Ca/As molar ratio is 5/3. If the molar ratio of Ca/As is 1.7 or less, the recovery rate of As decreases, and if it is 2.0 or more, unreacted slaked lime remains As impurities, which is not preferable.
Further, as shown in the above reaction formula [2], since calcium arsenate is produced together with sodium hydroxide, sodium hydroxide contained in the filtrate obtained by subjecting calcium arsenate to solid-liquid separation is returned to the above oxidation leaching step and can be reused as an alkali source.
In the calcium arsenate generation step, the solution preferably has a pH of 7.5 to 11, and more preferably a pH of 9 to 10. If the pH is less than 7.5, the regenerated sodium hydroxide concentration decreases as shown in the following formula [3], and if the pH is 11 or more, the formation of calcium arsenate is insufficient, which is not preferable.
3NaH2AsO4+5Ca(OH)2＝3NaOH+As3Ca5O13H↓+6H2O [3]
The solution temperature in the calcium arsenate generation step is preferably 50 to 70 ℃. If the solution temperature is less than 50 ℃, calcium arsenate is not sufficiently produced. When the solution temperature exceeds 70 ℃, crystalline calcium arsenate grows around calcium hydroxide to inhibit the reaction, which is not preferable. The heating time is preferably 1 to 4 hours.
[ vitrification of calcium arsenate ]
A vitrified material containing iron, silica and an alkaline component is added to calcium arsenate so that the weight ratio of iron to silica is 0.5 to 0.9 and the amount of alkaline component is 14 to 26 wt%, thereby producing a glass-cured product of calcium arsenate.
The weight ratio of iron to silica is the ratio of the weight of iron contained in the vitrified material to the weight of silica contained in the vitrified material.
The weight percentage of the amount of the basic component is the percentage of the weight of the basic component relative to the total weight of the dry weight of calcium arsenate and the weight of the vitrified material.
The weight in this specification is used in the same sense as the mass. Thus, the weight ratio is a mass ratio, and the weight% is a mass%.
As the vitrification material containing iron, silica and an alkali component, for example, waste glass and copper slag containing iron, silica, calcium and sodium can be used. The waste glass and the copper slag may be used in a mixture with silica sand or the like as a silica source so that the weight ratio of iron to silica and the amount of alkali component in the present invention fall within the ranges. Furthermore, the waste glass and the copper slag may be mixed for use.
A glass-solidified material is produced by mixing and heating and melting a vitrification material and calcium arsenate so that the weight ratio of iron to silica (Fe/SiO2) of the glass-solidified material is 0.5 to 0.9 and the amount of an alkaline component is 14 to 26 wt%.
The iron component and the silica component of the glass solidified body are the iron component and the silica component mainly contained in the vitrified material. The alkali component of the solidified glass is a Ca component of calcium arsenate, and a Ca component and a Na component contained in the vitrification material. The amount of the alkali component is the total amount of oxides of the alkali component, and in the glass solidified body containing sodium and calcium as the alkali component, the amount of the alkali component is Na2Total amount of O and CaO.
If the glass-solidified body has a weight ratio of iron to silica (Fe/SiO)2) If the amount of arsenic eluted is less than 0.5 or exceeds 0.9, the amount of arsenic eluted exceeds an environmental standard (0.3ppm) in the elution test of the glass-solidified body (elution test according to environmental Notification No. 13). And, if the amount of alkali component of the glass-solidified body is Na, for example2When the total amount of O and CaO is less than 14 wt%, the arsenic concentration is less than 5 wt%, and the economic advantage is reduced, and if Na is used2When the total amount of O and CaO exceeds 26 wt%, the arsenic concentration becomes 15 wt% or more, and the elution amount of arsenic increases, which is not preferable.
The upper limit of the heating temperature in the vitrification step is preferably 1400 ℃. When the heating temperature is 1450 ℃ or higher, the arsenic oxide volatilizes due to decomposition of calcium arsenate, and the arsenic cannot be fixed. On the other hand, the lower limit of the heating temperature is a temperature at which a mixture of calcium arsenate and a vitrification material melts. The temperature in the vitrification step may be usually 1000 to 1400 ℃ and preferably 1100 to 1350 ℃. The heating and melting time is about 15 to 30 minutes. The heating method is not limited as long as the heating temperature is set as described above. In general, a melting furnace or the like can be used.
The arsenic-containing glass solidified body produced by the arsenic fixing method according to the present invention may have an arsenic concentration of 5 wt% or more and 15 wt% or less. If the arsenic concentration of the glass-solidified body is less than 5% by weight, the economic advantage is small. On the other hand, in order to make the arsenic concentration of the solidified glass exceed 15 wt%, calcium arsenate having a CaO concentration of 26 wt% or more needs to be used, and since the CaO concentration of the solidified glass also becomes high and exceeds the range of the amount of the alkali component in the treatment method according to the present invention, the elution amount of arsenic increases.
Hereinafter, examples and comparative examples of the treatment method and the arsenic-containing glass solidified body according to the present invention will be described together.
[ example 1]
100g (dry mass) of copper arsenide-containing sludge (30 wt% As and 60 wt% Cu) was mixed with 0.5L of caustic soda solution (65 g/L NaOH concentration), and the mixture was heated to 85 ℃ with stirring, and oxidation leaching was performed while blowing air for 1L/min. The leachate is subjected to solid-liquid separation, and the sodium arsenate solution is recovered. To 500ml of this sodium arsenate solution (As: 39g/L, pH10, 50 ℃) was added 32g of hydrated lime and the mixture was stirred for 4 hours to form a white precipitate (calcium arsenate precipitate). The resulting slurry was subjected to solid-liquid separation to recover 64g (dry mass) of a calcium arsenate precipitate (30% by weight of As and 35% by weight of Ca) and 500ml of a filtrate (20 ppm of As and 41g/l of NaOH).
In the weight ratio of iron to silicon dioxide and the amount of alkaline component (Na)2Total amount of O and CaO) to the values of Table 1, was returnedAnd adding a vitrification material mixed with copper slag and silica sand into the collected calcium arsenate to prepare a mixed sample. The mixed sample was placed in a crucible, and heated at 1350 ℃ under atmospheric pressure for 30 minutes to be melted. The melt was cooled and the glass solidified body was recovered. The glass solidified body was subjected to an arsenic elution test (according to environmental note No. 13). The compositions of the glass-solidified bodies and the results of the arsenic elution test are shown in Table 1 (sample Nos. 1 to 6).
As shown in Table 1, samples Nos. 1 to 6 of this example are each limited as follows: the weight ratio of iron to silica is in the range of 0.5 to 0.9, the amount of alkaline component is in the range of 14 to 26 wt%, and the amount of arsenic eluted is 0.28ppm or less.
[ Table 1]
[ example 2]
The calcium arsenate recovered in example 1 was treated with a mixture of copper slag and waste glass as a vitrification material in such a manner that the weight ratio of iron to silica and the amount of alkali component (Na) were set2Total amount of O and CaO) was added to the glass transition material so as to have a value of table 1, thereby preparing a mixed sample. The mixed sample was placed in a crucible, and heated at 1350 ℃ under atmospheric pressure for 30 minutes to be melted. The melt was cooled and the glass solidified body was recovered. The glass solidified body was subjected to an arsenic elution test (according to environmental note No. 13). The composition of the glass solidified body and the results of the arsenic elution test are shown in Table 2 (sample No. 21).
As shown in Table 2, sample No.21 of this example is limited as follows: the weight ratio of iron to silica is in the range of 0.5 to 0.9, the amount of alkaline component is in the range of 14 to 26 wt%, and the amount of arsenic eluted is 0.3ppm or less.
[ Table 2]
[ comparative example 1]
The weight ratio of iron to silica and the amount of alkaline component (Na) in the calcium arsenate recovered in example 1 were measured using a copper slag without silica sand as a vitrification material2Total amount of O and CaO) was added to the steel slag so as to have a value shown in table 3, thereby preparing a mixed sample. This mixed sample was heated and melted in the same manner as in example 1, thereby producing a glass solidified body. The same arsenic elution test as in example 1 was performed with respect to this glass solidified body. The composition of the glass-solidified body and the arsenic elution test results are shown in table 3.
As shown in Table 3, since the amount of iron component is large in the copper slag used as a vitrification material, even if the weight ratio of iron to silica is 0.9 or more, the amount of alkaline component is in the range of 14 to 26 wt%, and the elution amount of arsenic exceeds 0.3ppm (sample Nos. 31 to 32).
[ comparative example 2]
The waste glass without copper slag was used as a vitrification material, and the weight ratio of iron to silica and the amount of alkali component (Na) were used in the calcium arsenate recovered in example 12Total amount of O and CaO) was added to the waste glass to have a value of table 3, thereby preparing a mixed sample. This mixed sample was heated and melted in the same manner as in example 1, thereby producing a glass solidified body. The same arsenic elution test as in example 1 was performed with respect to this glass solidified body. The composition of the glass-solidified body and the results of the arsenic elution test are shown in Table 3 (sample No. 33).
As shown in Table 3, since the amount of alkali components is large in the waste glass of the vitrified material, the amount of alkali components exceeds 26% by weight, and the amount of arsenic eluted exceeds 0.3 ppm.
[ comparative example 3]
Copper slag and waste glass were used as vitrification materials, and the weight ratio of iron to silica and the amount of alkaline component (Na) were used in the calcium arsenate recovered in example 12Total amount of O and CaO) was added to the waste glass to have a value of table 3, thereby preparing a mixed sample. The mixed sample was heated and melted in the same manner as in example 1 to produce glassAnd (5) curing the body. The same arsenic elution test as in example 1 was performed with respect to this glass solidified body. The composition of the glass-solidified body and the results of the arsenic elution test are shown in Table 3 (sample No. 34).
As shown in Table 3, even if the amount of the alkali component exceeds 26% by weight, the weight ratio of iron to silica is in the range of 0.5 to 0.9, and the elution amount of arsenic exceeds 0.3ppm (sample No. 34).
[ Table 3]
Industrial applicability
In electrolytic refining of copper, arsenic accumulated in an electrolytic solution can be easily fixed at low cost using a low-cost vitrification material such as copper slag and silica sand. As a result, arsenic can be concentrated and stored stably for a long period of time.
Claims (2)
1. A method for immobilizing arsenic, characterized in that,
adding a sodium hydroxide solution and an oxidizing agent to copper arsenide-containing sludge as a copper arsenic-containing material, heating the mixture to perform oxidation leaching to leach arsenic,
solid-liquid separation of the leaching residue, addition of slaked lime having a Ca/As molar ratio of 1.7 to 2.0 to the recovered sodium arsenate solution to produce calcium arsenate,
in the recovered calcium arsenate, the weight ratio of iron to silicon dioxide in the glass solidified body is 0.5-0.9, and Na is used2The calcium arsenate is formed into the glass solidified body by adding a vitrification material containing iron, silica and an alkali component so that the amount of the alkali component of the total amount of O and CaO is 14 to 26 wt% and the arsenic content is 11 to 15 wt%.
2. The method for immobilizing arsenic according to claim 1, wherein,
hydrated lime is added to a sodium arsenate solution to produce calcium arsenate, the solution containing the calcium arsenate is subjected to solid-liquid separation to recover the calcium arsenate, and a filtrate containing sodium hydroxide is returned to the oxidation leaching step and reused as an alkali source for the oxidation leaching.
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| PCT/JP2016/088108 WO2017110877A1 (en) | 2015-12-23 | 2016-12-21 | Method for immobilizing arsenic, and arsenic-containing vitrified waste |
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| US11168014B2 (en) * | 2018-04-30 | 2021-11-09 | Dundee Sustainable Technologies Inc. | System and method of fabrication of arsenic glass |
| CN110923457B (en) * | 2019-12-27 | 2021-06-04 | 中国科学院电工研究所 | Preparation method of high-purity arsenic crystal |
| CN113136489B (en) * | 2020-04-13 | 2022-07-15 | 中南大学 | Synchronous processing method for detoxifying and recycling high-arsenic soot |
| CN111575483B (en) * | 2020-04-17 | 2022-08-02 | 昆明铂锐金属材料有限公司 | Method for separating selenium, tellurium, arsenic, copper, lead and silver and enriching gold from copper anode slime |
| CN111533228A (en) * | 2020-05-19 | 2020-08-14 | 宁夏大学 | Method for treating arsenic-containing wastewater by hierarchical regulation and control and reducing and stabilizing arsenic slag |
| JP7565585B2 (en) | 2020-12-04 | 2024-10-11 | 株式会社キノテック | Zinc carbonate manufacturing method |
| CN112718793B (en) * | 2020-12-15 | 2022-03-11 | 紫金矿业集团股份有限公司 | Method for directly vitrifying arsenic-fixing material containing arsenite |
| CN112919801B (en) * | 2021-02-23 | 2022-03-15 | 浙江本尊新材料科技有限公司 | Method for preparing arsenic-containing borosilicate glass by arsenic solid waste treatment |
| CN114920529A (en) * | 2022-05-31 | 2022-08-19 | 湖南现代环境科技股份有限公司 | Composite curing agent and treatment process of arsenic-containing waste residue |
| CN116197209A (en) * | 2023-01-17 | 2023-06-02 | 广西凯玺有色金属有限公司 | Cleaning treatment method for calcium arsenate glass solidification and application thereof |
| CN116217075B (en) * | 2023-03-02 | 2024-08-06 | 广东飞南资源利用股份有限公司 | Regulation and control slag and regulation and control method for vitrification treatment of dangerous solid wastes |
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| US10758954B2 (en) | 2020-09-01 |
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| WO2017110877A1 (en) | 2017-06-29 |
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| JP6691680B2 (en) | 2020-05-13 |
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